BMP ID: |
4465 |
Title: |
Pipe Glycol Dehydrator Vapor to VRU. |
Text: |
Table 1â€"Cost-Effective Options for Reducing Methane Emissions: "Pipe Glycol Dehydrator Vapor to VRU. Another option for reducing methane, VOC, and HAP emissions from a glycol dehydrator is to pipe the regenerator vent stack to an oil-storage tank equipped with a vapor-recovery unit (VRU). The vapor space in the tank serves as a cushion for variations in pressure and flow from the dehydrator and oil production. Additional gas recovery enhances the economics of a VRU. The VRU boosts the recovered gas pressure enough to inject it into a fuel-gas system, compressor-suction, or gathering/sales line." [see Table 2 and 3 in the source document for costs, benefits, and production characteristics] |
Source Publication Name: |
Cost-effective methane emissions reductions for small and midsize natural gas producers |
Citation Section: |
Table 1 |
Citation Page: |
3 |
Supplemental Documents: |
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Usage Type: |
Recommended |
Timing: |
• Production / Operation / Maintenance
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Oil / Gas Field: |
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Surface Ownership: |
• Federal
• State
• Private
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Mineral Ownership: |
• Federal
• State
• Private
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Primary Contact: |
Environmental Protection Agency Ariel Rios Building, 1200 Pennsylvania Avenue, N.W. Washington, DC 20460 United States |
Phone: | (202) 272-0167 |
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Alt. Phone: | (202) 272-0165 |
Fax: | |
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E-mail: | |
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Alternate Contact: |
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Categories: |
Air Quality and Emissions
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Location: |
General / Federal |
Species: |
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Vegetation Types: |
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General Comments: |
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Cost-Benefit Analysis: |
Cost & Benefits :
Equipment Cost =
$1000;
O&M Cost =
$3000;
Saleable Gas Saving (Mcf/d) =
9.0;
Expected Payback =
Less than a year. (Price assumption $5/Mcf);
Operating Requirement =
Existing VRU with excess capacity;
Basis for cost saving =
Dehydrator throughput = 10 MMcfd.
operating cost is incremental electricity;
Other Benefits =
More gas for sale of fuel. |
BMP Efficacy: |
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Date Entered: |
2009-04-08 08:27 UTC |
Last Updated: |
2011-07-17 13:53 UTC |